EP4658613A1

EP4658613A1 - A process for producing carbon impurity reduced/carbon impurity free lithium sulfide, said carbon impurity reduced/carbon impurity free lithium sulfide, and its use for producing solid electrolytes and solid batteries

Info

Publication number: EP4658613A1
Application number: EP23821634.5A
Authority: EP
Inventors: Ulrich Wietelmann; Alexander Huebner; Katrin Wessels; Thomas Jansen; Anja Weiland; Tannita Frommer; Raphael Steinbach
Original assignee: Albemarle Germany GmbH
Current assignee: Albemarle Germany GmbH
Priority date: 2023-02-01
Filing date: 2023-12-11
Publication date: 2025-12-10
Also published as: DE102023102404A1; WO2024160430A1; CN120603781A; KR20250142295A; TW202432452A; JP2026503768A

Abstract

The invention relates to a process for the production of lithium sulfide reduced in carbon impurity or free from carbon impurity, in which lithium sulfide containing carbon impurity is treated with hydrogen gas in a temperature range from 450 to 1000 ° C. The invention further relates to a lithium sulfide producible in this manner, the carbon impurity content of which is less than 0.3% by weight based on the weight of the lithium sulfide. This lithium sulfide is used for the production of battery components, preferably solid electrolytes, and solid-state batteries.

Description

A process for producing carbon impurity reduced/carbon impurity free lithium sulfide , said carbon impurity reduced/carbon impurity free lithium sulfide , and its use for producing solid electrolytes and solid batteries

The invention relates to a method for the preparation of lithium sulfide reduced in carbon impurity or free from carbon impurity or for purifying lithium sulfide to efficiently remove impurities such as residual carbon or other carbon-containing impurities from lithium sulfide , respecitvely, used for electronic and electrical materials . Furthermore , the invention relates to said purified lithium sulfide , a solid electrolyte for a rechargeable lithium battery and a solid battery containing such a solid electrolyte .

Lithium sulfide is currently attracting much interest as a raw material for the preparation of solid electrolytes for solid- state batteries (Lee et . al , Acc . Chem . Res , 54 , 3390 , 2021 ) . Solid-state batteries offer higher energy densities and faster charging capabilities compared to the state of the art . In addition, solid-state batteries are generally considered safer because they do not contain highly flammable organic solvents (Lee et . al , Acc . Chem . Res , 54 , 3390 , 2021 ) . In addition, lithium sulfide finds application as a cathode material in lithium/sulf ur batteries ( EP 2 896 085 Al ) . Lithium/sulfur batteries also have a significantly higher energy density compared to conventional lithium-ion batteries and are thus of interest for potential application in the field of electromobility .

I f the purity level of a raw material , such as a solid electrolyte used in a rechargeable battery, is low, component aging can accelerate . Therefore , the purity level of the solid electrolyte or other raw material must be high ( EP 1 681 263 Al ) . In particular , graphiti zed carbon in lithium sulfide as a raw material for solid electrolytes must be avoided as completely as possible , since it can lead to undesirable electronic conductivity in the solid electrolyte (Nikodimos et . al , Energy Environ . Sci . , 2022 , 15 , 991 ) . Processes for the preparation of lithium sulfide , by which lithium sulfide can be prepared by simple means , are sufficiently known ( e . g . , EP 0 802 575 Al ) .

One known process describes the production of lithium sulfide in a carbothermic reduction at high temperatures from lithium sulfate and carbon ( CN 106229487 A) . It is basically an economical and simple process , since the production steps can also be carried out continuously . In addition, the raw materials lithium sulfate and carbon are readily available . However, carbothermal reduction often leads to significant impurities in the lithium sulfide . These are usually unreacted reactants such as carbon or lithium sulfate . In addition , lithium sulfite , lithium carbonate , and/or lithium oxide may be formed .

Another process describes the reduction of lithium sulfate with hydrogen to lithium sulfide at high temperatures ( US-A 2 840 455 ) . A disadvantage here is the very slow reaction rate to lithium sulfide . Although the reaction rate can be significantly increased by raising the temperature , it leads to the formation of a melt which solidifies after cooling and does not result in the desired powdered lithium sul fide . These circumstances make reduction with hydrogen to lithium sulfide economically unattractive .

I f lithium sulfide is produced by the carbothermic method, the typical contamination with residual carbon causes the lithium sulfide to produce additional undesirable electronic conductivity as a raw material for a solid electrolyte for a rechargeable lithium battery, and thus the desired battery performance and long-term stability cannot be achieved .

It is an obj ect of the invention to solve this problem by providing a process for producing lithium sulfide reduced in carbon impurity or free from carbon impurity, in which a content of carbon and/or carbonaceous impurities contained in the lithium sulfide constituting a raw material for a solid electrolyte of a rechargeable lithium battery is minimi zed or completely avoided . Another obj ect of the invention is to provide such lithium sulfide reduced in carbon impurity or free of carbon impurity, a solid electrolyte , in particular for a rechargeable lithium ion battery, using such lithium sulfide , and a solid battery in which the carbon impurities are minimal or absent .

These obj ects are solved by a process for producing lithium sulfide reduced in carbon impurity or free from carbon impurity, characteri zed in that lithium sulf ide containing carbon impurity is treated with hydrogen gas in a temperature range of 450 to 1000 °C .

The invention therefore provides lithium sulfide that is low or free of carbon impurities , which is produced by this process according to the invention .

Furthermore , the invention relates to the use of such a lithium sulfide for the production of battery components , preferably in solid electrolytes .

Accordingly, the invention also relates to a process for purifying lithium sulfide that can efficiently remove impurities such as residual carbon or other carbonaceous impurities from lithium sulfide .

Furthermore , the invention relates to such a solid electrolyte for a rechargeable lithium ion battery and a corresponding solid battery .

Surprisingly, it has been shown according to the invention that carbon impurities , e . g . excess carbon or carbon-containing , inorganic or organic compounds in the lithium sulfide can be removed by a specific post-treatment with hydrogen at high temperatures without the disadvantages expected in the prior art .

The residual carbon/residual carbon compound content of the lithium sulfide treated with hydrogen gas according to the invention is less than 0 . 3% by weight , preferably less than 0 . 2 % by weight and in particular less than 0 . 1% by weight . Ideally, it is 0 wt% . The lithium sulfide used for the production of carbon impurity reduced/carbon impurity free lithium sulfide according to the invention is preferably produced carbothermal by first reducing lithium sulfate with a carbon source, preferably carbon black, to lithium sulfide.

Carbon sources or carbon impurities can include crystalline and amorphous forms of carbon. Crystalline forms include graphite, graphite-like carbon (including carbon black or activated carbon) , graphene, fullerenes, or carbon nanotubes. Carbonaceous impurities include both inorganic carbon compounds (e.g. , carbides) and organic carbon compounds.

In order to produce a lithium sulf ate/carbon mixture that is as homogeneous as possible, the two components are preferably mixed in a zirconium dioxide-lined plane ball mill. For better mixing, zirconium dioxide balls can also be added to the grinding bowl. The grinding time is typically between 1 and 24 hours, preferably 1 to 3 hours.

The lithium sulf ate/carbon mixture is typically reacted in the temperature range from 650 to 900°C under inert conditions, preferably in the temperature range from 750 to 850°C. For the purposes of the invention, inert conditions are understood to mean working under inert gas to the exclusion of air and humidity. For this purpose, the lithium sulf ate/carbon mixture is weighed out, mixed as homogeneously as possible, filled into a temperature-resistant crucible, e.g. aluminum oxide, boron nitride or glassy carbon, and reacted according to the following reaction equation:

Li₂SO₄ + (2+x) C Li₂S + x C + 2 CO₂ (x = 0 bis 2) where x represents excess carbon.

The lithium sulf ate/carbon molar ratio is therefore in the range 1:2 to l:2+x, with x = 0 to 2, preferably, based on lithium sulfate, a stoichiometric excess carbon in the range 1 - 10 wt . % is present, even more preferably a stoichiometric excess carbon in the range 1 - 5 wt . % . This reaction results in a lithium sulfide contaminated with carbon. Due to inhomogeneities in the starting mixture, undesirable residual carbon usually cannot be completely avoided .

The problem is solved by the step of purifying the lithium sulfide according to the invention as follows:

According to the invention, the contaminated lithium sulfide is treated with a hydrogen-containing gas mixture, where the hydrogen content can be from 1 to 100% by volume, preferably from 5 to 10% by volume, the remainder of the hydrogen gas being nitrogen and/or argon.

The treatment with the hydrogen gas according to the invention is carried out in a temperature range of 450 to 1000 °C, preferably 650 to 1000°C, preferred 750 to 1000°C, more preferred 800 to 1000°C, still more preferred 800 to 950°C, in particular 800 to 900°C.

The treatment time with the hydrogen gas according to the invention is in particular 1 to 10 hours, preferably 1 to 8 hours, preferred 1 to 5 hours. For this purpose, commercially available "forming gases", i.e. mixtures of hydrogen and nitrogen and/or argon, can be used, for example.

According to the invention, the lithium sulfide contaminated with carbon can be treated for example according to the equation below, at 800 to 1000°C with forming gas containing 5% hydrogen by volume for 1 to 10 hours. The amount of He required is at least twice the stoichiometric amount of the residual carbon :

Li₂S + x C + 2x H₂ - Li₂S + CH₄ .

According to the reaction equation, the remaining carbon is removed from the lithium sulfide in this reaction by the formation of gaseous methane. What remains is purified white crystalline lithium sulfide. The exemplary isolated material shows lines in the X-ray diffraction pattern only for the desired Li2S (content >99 wt%) , the carbon content is < 0.3 wt%. According to the invention, the lithium sulfide is preferably overflowed with a stream of the hydrogen gas during the treatment .

Preferably, the lithium sulfate used is high-purity, anhydrous lithium sulfate obtained from lithium-containing minerals such as spodumene , brines or from recycled lithium ion batteries . Carbon black with a specific surface area of 1 to 1000 m²/g, preferably 100 to 200 m²/g, is used as the carbon source .

Measurement methods

The phase purity of the samples was checked using a Bruker D2-Phaser X-ray powder diffractometer in Bragg-Brentano geometry . An X-ray tube with Cu-Ka radiation ( A = 0 . 15418 nm) was used as the radiation source .

Quantification of lithium, sulfur , and carbon in lithium sulfide was performed using the elemental analysis unit of the Keyence VHX-7000 digital microscope . Using a UV laser ( A = 250 nm; P = 0 . 01 mW) , a small amount of sample ( < 1 mg ) is vapori zed and atomi zed . The characteristic atomic emission lines are detected and used for quantification .

The body color of the samples obtained was determined using RAL comparison cards from RAL GmbH . Using these standardized color charts , the respective CIELAB color coordinates can be determined .

The advantages of the process according to the invention compared to the state of the art are thus :

• the direct purification of a lithium sulfide obtained by carbothermal reduction and the resulting availability of the low-carbon/carbon-f ree lithium sulfide for the production of solid-state electrolytes ;

• the use of commercially readily available starting materials ; • the avoidance of working with air and moisture sensitive solids such as Li-metal, lithium hydride, lithium alkyls, lithium aryls or lithium amides;

• avoidance of working with toxic sulfur sources, such as hydrogen sulfide or carbon disulfide;

• direct use of lithium sulfate from lithium ion battery recycling without the energy-intensive conversion to, for example, lithium hydroxide;

• the avoidance of organic solvents (e.g. THF) for further purification of the lithium sulfide by a further process step .

All operations are preferably performed in an Ar-filled glove box.

The measurement methods described above were used in the following Examples to determine the product properties.

Examples

Example 1 :

4.4 g (40 mmol) of lithium sulfate (99.0%, Albemarle Germany GmbH) , anhydrous with 0.96 g (80 mmol) of carbon black with a specific surface area of about 176 m²/g (Cabot Vulcan P Fluffy) were weighed in and then intimately triturated in an agate mortar.. The lithium sulf ate/carbon mixture was then transferred to a Fritsch zirconium dioxide lined grinding bowl. 12 grinding balls with a diameter of 10 mm were added. The grinding bowl was then hermetically sealed under inert gas and placed in the Pulverisette 7 planetary ball mill from Fritsch. The mixture was ground for 2 hours at 600 rpm. After the grinding process, the zirconium dioxide balls were sieved off. The homogenized lithium sulfate/carbon mixture was then transferred to a corundum annealing box. The mixture was converted to lithium sulfide for 3.3 hours at 850°C under a stream of nitrogen. The lithium sulfide, still contaminated with carbon, was then post-treated by switching to forming gas containing 5% hydrogen by volume for 6 hours at 900°C. After cooling, it was purged with nitrogen. The purified lithium sulfide had lost its gray discoloration, due to residual carbon, and was pure white. In addition, phase purity was checked by X-ray diffraction. The lithium sulfide obtained was a microcrystalline powder, which shows no sintering or other agglomerates.

Content Li2S: > 99

Residual carbon content: < 0.3%

Color Li2S : Pure white

Color coordinate CIELAB: L = 94.57 ; a = -0.47 ; b = 4.14

Example 2 :

4.4 g (40 mmol) of lithium sulfate (99.0%, Albemarle Germany GmbH) , anhydrous with 0.96 g (80 mmol) of carbon black with a specific surface area of about 176 m²/g (Cabot Vulcan P Fluffy) were weighed in and then intimately triturated in an agate mortar. The lithium sulf ate/carbon mixture was then transferred to a Fritsch zirconium dioxide lined grinding bowl. 12 grinding balls with a diameter of 10 mm were added. The grinding bowl was then hermetically sealed under inert gas and placed in the Pulverisette 7 planetary ball mill from Fritsch. The mixture was ground for 20 hours at 600 rpm. After the grinding process, the zirconium dioxide balls were sieved off. The homogenized lithium sulfate/carbon mixture was then transferred to a corundum annealing box. The mixture was converted to lithium sulfide for 8 hours at 800°C under a stream of nitrogen. The lithium sulfide, still contaminated with carbon, was then post-treated by switching to forming gas containing 5% hydrogen by volume for 8 hours at 850°C. After cooling, it was purged with nitrogen. The purified lithium sulfide had lost its gray discoloration, due to residual carbon, and was pure white. In addition, phase purity was checked by X-ray diffraction. The lithium sulfide obtained was a microcrystalline powder, which shows no sintering or other agglomerates .

Content Li2S: > 99 Residual carbon content: < 0.3%

Color Li2S: Pure white

Color coordinate CIELAB: L = 94.57 ; a = -0.47 ; b = 4.14

Comparative Example 1: Conversion without H2 post-treatment.

4.4 g (40 mmol) lithium sulfate (99.0%, Albemarle Germany GmbH) , anhydrous with 0.96 g (80 mmol) carbon black with a specific surface area of about 176 m²/g (Cabot Vulcan P Fluffy) were weighed in and then intimately triturated in an agate mortar. The lithium sulf ate/carbon mixture was then transferred to a Fritsch zirconium dioxide lined grinding bowl. 12 grinding balls with a diameter of 10 mm were added. The grinding bowl was then hermetically sealed under inert gas and placed in the Pulverisette 7 planetary ball mill from Fritsch. The mixture was ground for 2 hours at 600 rpm. After the grinding process, the zirconium dioxide balls were sieved off. The homogenized lithium sulf ate/carbon mixture was then transferred to a corundum annealing box. The mixture was converted to lithium sulfide for

3.3 hours at 850°C under a stream of nitrogen.

Content Li2S: 95%

Residual carbon content: 5%

Color Li2S : Pearl dark gray

Color coordinate CIELAB: L = 57.32 ; a = -0.31 ; b = -0.98

Comparative Example 2: Conversion without H2 post-treatment.

4.4 g (40 mmol) lithium sulfate (99.0%, Albemarle Germany GmbH) , anhydrous with 0.96 g (80 mmol) carbon black with a specific surface area of about 176 m²/g (Cabot Vulcan P Fluffy) were weighed in and then intimately triturated in an agate mortar. The lithium sulf ate/carbon mixture was then transferred to a Fritsch zirconium dioxide lined grinding bowl. 12 grinding balls with a diameter of 10 mm were added. The grinding bowl was then hermetically sealed under inert gas and placed in the Pulverisette 7 planetary ball mill from Fritsch. The mixture was ground for 20 hours at 600 rpm. After the grinding process, the zirconium dioxide balls were sieved off. The homogenized lithium sulf ate/carbon mixture was then transferred to a corundum annealing box. The mixture was converted to lithium sulfide for 8 hours at 800°C under a stream of nitrogen.

Content Li₂S: 97%

Residual carbon content: 3%

Color Li2S: Pearl light gray

Color coordinate CIELAB: L = 65.38 ; a = -0.43 ; b = -0.34

Example 3 :

Preparation of the solid state electrolyte LiePSsCl

2.140 g (46.57 mmol) of the lithium sulfide prepared in embodiment Example 1, 2.070 g (9.312 mmol) of phosphorpentasulfide (99%, Sigma Aldrich) and 0.790 g (18.6 mmol) of lithium chloride (Battery Grade, Albemarle Germany GmbH) were weighed in and then triturate intimately. The mixture was then transferred to a Fritsch zirconium dioxide lined grinding bowl. 12 grinding balls with a diameter of 10 mm were added. The grinding bowl was then hermetically sealed under inert gas and placed in the Pulverisette 7 planetary ball mill from Fritsch. The mixture was ground at 600 rpm for 20 hours. After the grinding process, the zirconium dioxide balls were removed. The homogenized mixture was then transferred to a metal cylinder and sealed with a screw cap. After 48 hours at 370°C in the chamber furnace, the conversion to the solid state electrolyte LigPSsCl was completed. The phase purity of the solid state electrolyte was checked by X-ray powder diffraction.

Claims

1. A process for the preparation of lithium sulfide reduced in carbon impurity or free from carbon impurity, characterized in that lithium sulfide containing carbon impurity is treated with hydrogen gas in a temperature range of 450 to 1000°C.

2. The process according to claim 1, characterized in that the carbon impurity is carbon or one or more carbon-containing, inorganic or organic compounds.

3. The process according to claim 1 or 2, characterized in that the content of carbon impurity of the lithium sulfide to be treated, based on the weight of the lithium sulfide, is 0.5 to 10, preferably 0.5 to 5% by weight.

4. The process according to one of the preceding claims, characterized in that the carbon impurity content of the lithium sulfide treated with the hydrogen gas after the treatment, based on the weight of the treated lithium sulfide, is less than 0.3% by weight, preferred less than 0.2% by weight, in particular less than 0.1% by weight, particularly preferred 0% by weight.

5. The process according to one of the preceding claims, characterized in that the hydrogen content of the hydrogen gas is 1 to 100% by volume, preferably 5 to 10% by volume, the remainder of the hydrogen gas being nitrogen and/or argon .

6. The process according to one of the preceding claims, characterized in that the treatment with the hydrogen gas is carried out at 650 to 1000°C, preferably 750 to 1000°C, preferred 800 to 1000°C, more preferred 800 to 950°C, still more preferred 800 to 900°C.

7. The process according to one of the preceding claims, characterized in that the treatment time with the hydrogen gas is 1 to 10 hours, preferably 1 to 8 hours, in particular 1 to 5 hours .

8. The process according to one of the preceding claims, characterized in that the lithium sulfide to be treated with the hydrogen gas is prepared by reaction of lithium sulfate with a carbon source, preferably carbon black, the molar lithium sulf ate/carbon ratio being in the range 1:2 to l:2+x, with x = 0 to 2, preferably a stoichiometric carbon excess in the range 1 - 10 wt. %, even more preferred a stoichiometric carbon excess in the range of 1 - 5 wt.%, based on lithium sulfate is used.

9. Lithium sulfide, characterized in that the content of carbon impurity of a carbothermal produced lithium sulfide, based on the weight of the lithium sulfide, is less than 0.3% by weight, preferably less than 0.2% by weight, in particular less than 0.1% by weight, and ideally is 0% by weight.

10. Lithium sulfide producible by the process as defined in any one of claims 1 to 8.

11. Use of carbon reduced/carbon free lithium sulfide as defined in claim 9 or 10 for the production of battery components, preferably in solid electrolytes.

12. Solid electrolyte, in particular for a rechargeable lithium ion battery, comprising lithium sulfide as defined in claim 9 or 10.

13. Solid battery comprising a solid electrolyte according to claim 12.